CN101818379B - Flax fibers and preparation method thereof - Google Patents
Flax fibers and preparation method thereof Download PDFInfo
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- CN101818379B CN101818379B CN2009100092835A CN200910009283A CN101818379B CN 101818379 B CN101818379 B CN 101818379B CN 2009100092835 A CN2009100092835 A CN 2009100092835A CN 200910009283 A CN200910009283 A CN 200910009283A CN 101818379 B CN101818379 B CN 101818379B
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- 235000004431 Linum usitatissimum Nutrition 0.000 title claims abstract description 332
- 239000000835 fiber Substances 0.000 title claims abstract description 315
- 238000002360 preparation method Methods 0.000 title claims abstract description 39
- 240000006240 Linum usitatissimum Species 0.000 title description 5
- 241000208202 Linaceae Species 0.000 claims abstract description 327
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 101
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 39
- 238000005554 pickling Methods 0.000 claims abstract description 33
- 230000003647 oxidation Effects 0.000 claims abstract description 30
- 238000005406 washing Methods 0.000 claims abstract description 12
- 238000010009 beating Methods 0.000 claims abstract description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 125
- 239000003921 oil Substances 0.000 claims description 67
- 235000019198 oils Nutrition 0.000 claims description 67
- 239000000839 emulsion Substances 0.000 claims description 44
- 239000003599 detergent Substances 0.000 claims description 41
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 40
- 229920000742 Cotton Polymers 0.000 claims description 36
- 238000009960 carding Methods 0.000 claims description 36
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 36
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- 239000004202 carbamide Substances 0.000 claims description 27
- 230000001590 oxidative effect Effects 0.000 claims description 25
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 25
- 239000004115 Sodium Silicate Substances 0.000 claims description 24
- 229910052911 sodium silicate Inorganic materials 0.000 claims description 24
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 20
- 235000015112 vegetable and seed oil Nutrition 0.000 claims description 19
- 239000008158 vegetable oil Substances 0.000 claims description 19
- 244000025254 Cannabis sativa Species 0.000 claims description 18
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 claims description 18
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 claims description 18
- 235000009120 camo Nutrition 0.000 claims description 18
- 235000005607 chanvre indien Nutrition 0.000 claims description 18
- 238000010438 heat treatment Methods 0.000 claims description 18
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- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 18
- 239000002253 acid Substances 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 11
- 239000003795 chemical substances by application Substances 0.000 claims description 10
- 230000035484 reaction time Effects 0.000 claims description 8
- 239000010721 machine oil Substances 0.000 claims description 7
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- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 2
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- 229910052708 sodium Inorganic materials 0.000 claims description 2
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- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims 1
- 238000000034 method Methods 0.000 description 44
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 42
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- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 15
- 239000012535 impurity Substances 0.000 description 12
- 239000003814 drug Substances 0.000 description 11
- 240000008564 Boehmeria nivea Species 0.000 description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 10
- 230000018044 dehydration Effects 0.000 description 10
- 238000006297 dehydration reaction Methods 0.000 description 10
- 229940079593 drug Drugs 0.000 description 10
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- 238000001035 drying Methods 0.000 description 7
- 239000000084 colloidal system Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000004744 fabric Substances 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
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- 238000012805 post-processing Methods 0.000 description 5
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- 238000009991 scouring Methods 0.000 description 4
- 210000002268 wool Anatomy 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
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- 238000000578 dry spinning Methods 0.000 description 3
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- 229910021645 metal ion Inorganic materials 0.000 description 3
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- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- JVBXVOWTABLYPX-UHFFFAOYSA-L sodium dithionite Chemical compound [Na+].[Na+].[O-]S(=O)S([O-])=O JVBXVOWTABLYPX-UHFFFAOYSA-L 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
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- 238000010521 absorption reaction Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000001814 pectin Substances 0.000 description 2
- 235000010987 pectin Nutrition 0.000 description 2
- 229920001277 pectin Polymers 0.000 description 2
- XXQBEVHPUKOQEO-UHFFFAOYSA-N potassium superoxide Chemical compound [K+].[K+].[O-][O-] XXQBEVHPUKOQEO-UHFFFAOYSA-N 0.000 description 2
- 238000004321 preservation Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- HHVIBTZHLRERCL-UHFFFAOYSA-N sulfonyldimethane Chemical compound CS(C)(=O)=O HHVIBTZHLRERCL-UHFFFAOYSA-N 0.000 description 2
- ICLYJLBTOGPLMC-KVVVOXFISA-N (z)-octadec-9-enoate;tris(2-hydroxyethyl)azanium Chemical compound OCCN(CCO)CCO.CCCCCCCC\C=C/CCCCCCCC(O)=O ICLYJLBTOGPLMC-KVVVOXFISA-N 0.000 description 1
- MBDUIEKYVPVZJH-UHFFFAOYSA-N 1-ethylsulfonylethane Chemical compound CCS(=O)(=O)CC MBDUIEKYVPVZJH-UHFFFAOYSA-N 0.000 description 1
- DKUITGQKEJLOBE-UHFFFAOYSA-N 2-(2-phenylethylsulfonyl)ethylbenzene Chemical compound C=1C=CC=CC=1CCS(=O)(=O)CCC1=CC=CC=C1 DKUITGQKEJLOBE-UHFFFAOYSA-N 0.000 description 1
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- KEAYESYHFKHZAL-UHFFFAOYSA-N Sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 1
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- PYKYMHQGRFAEBM-UHFFFAOYSA-N anthraquinone Natural products CCC(=O)c1c(O)c2C(=O)C3C(C=CC=C3O)C(=O)c2cc1CC(=O)OC PYKYMHQGRFAEBM-UHFFFAOYSA-N 0.000 description 1
- 150000004056 anthraquinones Chemical class 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000001768 carboxy methyl cellulose Substances 0.000 description 1
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 206010061592 cardiac fibrillation Diseases 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000002738 chelating agent Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 210000002615 epidermis Anatomy 0.000 description 1
- 150000002191 fatty alcohols Chemical class 0.000 description 1
- 230000002600 fibrillogenic effect Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 235000021388 linseed oil Nutrition 0.000 description 1
- 239000000944 linseed oil Substances 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 239000002932 luster Substances 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
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- 239000007800 oxidant agent Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 229940051841 polyoxyethylene ether Drugs 0.000 description 1
- 229920000056 polyoxyethylene ether Polymers 0.000 description 1
- 229920000136 polysorbate Polymers 0.000 description 1
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000012312 sodium hydride Substances 0.000 description 1
- 229910000104 sodium hydride Inorganic materials 0.000 description 1
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 description 1
- PFUVRDFDKPNGAV-UHFFFAOYSA-N sodium peroxide Chemical compound [Na+].[Na+].[O-][O-] PFUVRDFDKPNGAV-UHFFFAOYSA-N 0.000 description 1
- 239000001488 sodium phosphate Substances 0.000 description 1
- 229910000162 sodium phosphate Inorganic materials 0.000 description 1
- 229910052979 sodium sulfide Inorganic materials 0.000 description 1
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 1
- 235000010265 sodium sulphite Nutrition 0.000 description 1
- 235000019832 sodium triphosphate Nutrition 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 229940117013 triethanolamine oleate Drugs 0.000 description 1
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
Abstract
本发明涉及一种亚麻纤维,所述亚麻纤维强度为3.0~8.0cN/dtex、细度为1500~3500公支;优选为强度4.0~7.0cN/dtex、细度为1500~3000公支;更优选为强度4.5~6.5cN/dtex、细度为1800~2800公支;最优选为强度5.0~6.0cN/dtex、细度为2300~2700公支。本发明还涉及所述的亚麻纤维的制备方法,包括浸酸、水洗、氧化、打纤、给油、脱油水、软麻、给油加湿、堆仓和机械开松步骤。本发明提供的亚麻纤维强度、细度高,制备方法工序短,污染小。The invention relates to a flax fiber. The flax fiber has a strength of 3.0-8.0 cN/dtex and a fineness of 1500-3500 branch; preferably, the strength is 4.0-7.0 cN/dtex and the fineness is 1500-3000 branch; moreover Preferably, the strength is 4.5-6.5cN/dtex, and the fineness is 1800-2800 branch; most preferably, the strength is 5.0-6.0cN/dtex, and the fineness is 2300-2700 branch. The invention also relates to the preparation method of the flax fiber, which comprises the steps of pickling, water washing, oxidation, beating, oiling, deoiling water, softening, oiling and humidifying, stacking and mechanical opening. The flax fiber provided by the invention has high strength and fineness, short preparation process and little pollution.
Description
技术领域 technical field
本发明属于纺织领域,具体的说,本发明涉及一种亚麻纤维及其制备方法。 The invention belongs to the textile field, in particular, the invention relates to a flax fiber and a preparation method thereof. the
背景技术 Background technique
随着人们生活水平的提高,对服装面料的吸湿透气性、保健性、挺括性、绿色环保等时尚风格愈为关注,这促使人们加强了对天然纤维资源的再利用与开发。亚麻纤维是优良的纺织原料,其织物具有吸湿散热好、透气性佳、纹理自然、光泽柔和、挺括大方等独特风格,这使得它倍受消费者偏爱。 With the improvement of people's living standards, more and more attention is paid to fashion styles such as moisture absorption, breathability, health care, crispness, and green environmental protection of clothing fabrics, which prompts people to strengthen the reuse and development of natural fiber resources. Flax fiber is an excellent textile raw material. Its fabric has unique styles such as good moisture absorption and heat dissipation, good air permeability, natural texture, soft luster, crisp and generous, which makes it highly preferred by consumers. the
当前国内麻纺厂主要采用湿法纺纱方法,即先将亚麻打成麻(其细度粗,约200~300公支)通过梳理、针梳、粗纱等工序生产粗纱,然后粗纱再经过煮漂以进一步去除所含的胶质,再在湿态下喂入细纱机进行纺纱。其工艺流程为:梳成长麻→加湿养生→配麻→成条→长麻预并(或混条机)→并条→长麻粗纱→粗纱煮漂→湿纺细纱→干燥→后加工。这种工艺复杂,流程长,可纺支数低,一般成纱细度在15~36公支,对设备要求很高,且工作环境差,同时又是湿法加工,很难进行亚麻与其他纤维的混纺,且湿纺纱比较僵硬,难以针织应用,在高档次、多品种的纺织产品开发方面有很大的局限性。 At present, the domestic flax spinning factory mainly adopts the wet spinning method, that is, flax is first beaten into flax (the fineness is coarse, about 200-300 public branches) to produce roving through carding, needle combing, roving and other processes, and then the roving is boiled and bleached. In order to further remove the colloid contained, it is then fed into the spinning frame in a wet state for spinning. The process flow is: combing hemp → humidification and health preservation → blending hemp → sliver forming → long hemp pre-merging (or mixing machine) → drawing frame → long hemp roving → roving boiled and bleached → wet spinning spun yarn → drying → post-processing. This kind of process is complicated, the process is long, and the spinnable count is low. Generally, the yarn fineness is 15-36. It requires high equipment, and the working environment is poor. At the same time, it is wet processing, so it is difficult to process flax and other textiles. The blending of fibers, and the wet spinning is relatively stiff, which is difficult to apply in knitting, and has great limitations in the development of high-grade and multi-variety textile products. the
专利申请95109371采用了水洗——酸洗——煮练——水洗——氧漂——水洗的方法制备亚麻粗纱,其采用连二亚硫酸钠、硫化钠、蒽醌和氢氧化钠进行煮练,然后再用双氧水,并加入双氧水稳定剂和ED-8进行氧漂。其方法将煮练和氧漂分开进行,增加了生产环节。此外,煮练中使用了大量的氢氧化钠,废水处理比较麻烦,对环境污染严重;连二亚硫酸钠毒性大,生产过程中对工人损伤严重,且产品中的连二亚硫酸钠残留对消费者健康造成威胁。 Patent application 95109371 adopts washing—pickling—scouring—washing—oxygen bleaching—washing to prepare flax roving, which uses sodium dithionite, sodium sulfide, anthraquinone and sodium hydroxide for scouring, and then Then use hydrogen peroxide, and add hydrogen peroxide stabilizer and ED-8 for oxygen bleaching. In the method, scouring and oxygen bleaching are carried out separately, which increases the production links. In addition, a large amount of sodium hydroxide is used in scouring, and the waste water treatment is cumbersome and seriously pollutes the environment; sodium dithionite is highly toxic, causing serious damage to workers during the production process, and the residue of sodium dithionite in the product is harmful to the health of consumers. threaten. the
专利申请88102614则将煮练和漂白合二为一进行,其将亚麻打成麻后预酸,然后煮漂、给油,最后精干麻。其煮漂时加入氢氧化钾或氢化钠,使用的漂白剂为过氧化氢、过氧化钾或过氧化钠等过氧化物,以吐温、斯本或三乙醇胺油酸脂为表面活性剂,此外还加入了二甲砜、二乙砜或苯乙砜等作为促进剂。 Patent application 88102614 combines scouring and bleaching into one, and it beats flax into flax, pre-acids it, then boils it, oils it, and finally dries the flax. Potassium hydroxide or sodium hydride is added when it is boiled and bleached. The bleaching agent used is peroxides such as hydrogen peroxide, potassium peroxide or sodium peroxide, and Tween, Siben or triethanolamine oleate is used as a surfactant. In addition, dimethyl sulfone, diethyl sulfone or phenethyl sulfone are added as accelerators. the
专利申请200610031004对亚麻等原料和脱胶液按照1∶10-20的重量比混合,在30~100℃下脱胶1-5小时,然后水洗、上油、干燥即得可供纺织用的纤维。所述的脱胶剂可以为过氧化氢,并加入磷酸钠、三聚磷酸钠等作为螯合剂,以尿素为氢键破坏剂,加入水玻璃或羧甲基纤维素为抗沉积剂,以亚硫酸钠或亚硫酸氢钠为木质素去除剂。但该方法制备的纤维丝细度低,且纤维强度差,在纺织领域的应用具有很大局限性。 Patent application 200610031004 mixes flax and other raw materials with degumming solution in a weight ratio of 1:10-20, degumming at 30-100°C for 1-5 hours, then washing, oiling and drying to obtain fibers for textile use. The degumming agent can be hydrogen peroxide, add sodium phosphate, sodium tripolyphosphate, etc. as a chelating agent, use urea as a hydrogen bond breaker, add water glass or carboxymethyl cellulose as an anti-deposition agent, use sodium sulfite or Sodium bisulfite is a lignin remover. However, the fiber filaments prepared by this method have low fineness and poor fiber strength, so the application in the textile field has great limitations. the
上述方法制备的亚麻纤维细度低,只能应用于昂贵的特殊设备上进行纺纱。为了解决上述问题,可以对亚麻纤维进行精细化处理,使纤维的性能(尤其是细度、柔软度等)进一步完善,以实现纺纱流程缩短,生产效率提高,成纱质量改善,应用领域拓宽。 The flax fiber prepared by the above method has low fineness and can only be used for spinning on expensive special equipment. In order to solve the above problems, the flax fiber can be finely treated to further improve the performance of the fiber (especially fineness, softness, etc.), so as to shorten the spinning process, improve production efficiency, improve yarn quality, and broaden the application field. . the
发明内容 Contents of the invention
本发明目的之一在于提供一种亚麻纤维,本发明提供的亚麻纤维具有较高的细度和强度,可以在其它纺纱系统上进行纺纱。 One of the purposes of the present invention is to provide a flax fiber. The flax fiber provided by the present invention has higher fineness and strength, and can be spun on other spinning systems. the
本发明目的之二在于提供这种亚麻纤维的制备方法,本发明提供的制备方法操作简单,环境污染小。 The second object of the present invention is to provide a preparation method of the flax fiber. The preparation method provided by the present invention is simple to operate and has little environmental pollution. the
为了实现上述发明目的,本发明采用如下技术方案: In order to realize the foregoing invention object, the present invention adopts following technical scheme:
一种亚麻纤维,所述亚麻纤维强度为3.0~8.0cN/dtex、细度为1500~3500公支;优选为强度4.0~7.0cN/dtex、细度为1500~3000公支;更优选为强度4.5~6.5cN/dtex、细度为1800~2800公支;最优选为强度5.0~6.0cN/dtex、细度为2300~2700公支。 A flax fiber, the flax fiber has a strength of 3.0 to 8.0 cN/dtex and a fineness of 1500 to 3500 branch; preferably a strength of 4.0 to 7.0 cN/dtex and a fineness of 1500 to 3000 branch; more preferably the strength 4.5-6.5cN/dtex, fineness 1800-2800 branch; most preferably strength 5.0-6.0cN/dtex, fineness 2300-2700 branch. the
根据前面所述的亚麻纤维,其特征在于,根据要求,开松后纤维的长度可达到30~80mm。 According to the aforementioned flax fiber, it is characterized in that, according to requirements, the length of the fiber after opening can reach 30-80 mm. the
前面所述的亚麻纤维的制备方法,包括浸酸、水洗、氧化、打纤、给油、脱油水、软麻、给油加湿、堆仓和机械开松步骤,其特征在于,所述的氧化步骤为,每千克亚麻纤维用水8~12kg,先在水中加入碳酸钠或碳酸钾、硅酸钠、尿素和渗透剂JFC,加入量为加入后每升水含碳酸钠或碳酸钾2~6g、硅酸钠2~8g、 The preparation method of the aforementioned flax fiber comprises the steps of pickling, washing, oxidation, fibrillation, oiling, deoiling water, softening, oiling and humidification, stacking and mechanical opening, and is characterized in that the oxidation The steps are: 8-12kg of water per kilogram of flax fiber, first add sodium carbonate or potassium carbonate, sodium silicate, urea and penetrant JFC to the water, the amount added is 2-6g of sodium carbonate or potassium carbonate, silicon dioxide per liter of water after adding Sodium acid 2 ~ 8g,
尿素2~8g和渗透剂JFC1~4g,完全溶解后加入H2O2,H2O2加入量以纯H2O2计为加入后每升水含H2O23~12g;优选为每千克亚麻纤维用水10kg,每升水含碳酸钠或碳酸钾2~4g、硅酸钠3~5g、尿素3~5g、渗透剂JFC2g,H2O2加入量以纯H2O2计为加入后每升水含H2O23~8g。 2~8g of urea and 1~4g of osmotic agent JFC, add H 2 O 2 after complete dissolution, the amount of H 2 O 2 is calculated as pure H 2 O 2 after adding 3~12g of H 2 O 2 per liter of water; preferably per kilogram Flax fiber water 10kg, each liter of water contains 2~4g of sodium carbonate or potassium carbonate, 3~5g of sodium silicate, 3~5g of urea, 2g of penetrant JFC, the amount of H 2 O 2 added is calculated as pure H 2 O 2 per liter of water after adding Contains H 2 O 2 3~8g.
根据前面所述的制备方法,所述氧化步骤为将亚麻放入氧化液中,从室温匀速升温至70~100℃,升温时间控制在20~60min,氧化反应时间为2.0~4.0小时;优选为从室温匀速升温至70~90℃,升温时间控制在30~40min,氧化反应时间为1.0~3.0小时。 According to the above-mentioned preparation method, the oxidation step is to put flax in the oxidizing solution, raise the temperature from room temperature to 70-100°C at a constant speed, control the heating time at 20-60 minutes, and the oxidation reaction time is 2.0-4.0 hours; preferably The temperature is raised from room temperature to 70-90°C at a constant speed, the heating time is controlled at 30-40 minutes, and the oxidation reaction time is 1.0-3.0 hours. the
根据前面所述的制备方法,所述浸酸步骤为酸的浓度为1~3g/L,温度在35~70℃,浴比为1∶8~1∶12,浸酸时间为30~80min,优选为酸的浓度为1~2g/L,温度在40~50℃,浴比为1∶10,浸酸时间为40~60min。 According to the aforementioned preparation method, the pickling step is that the acid concentration is 1 to 3 g/L, the temperature is 35 to 70° C., the bath ratio is 1:8 to 1:12, and the pickling time is 30 to 80 minutes. Preferably, the acid concentration is 1-2g/L, the temperature is 40-50°C, the bath ratio is 1:10, and the pickling time is 40-60min. the
根据前面所述的制备方法,所述的给油步骤中油剂为机械油,优选为锭子油或白油;每千克亚麻纤维用机械油10~40g、用NaOH 1~8g、洗涤剂2~10g,与8~12kg水搅拌调制成乳化液,将亚麻纤维浸渍其中,在60~100℃的环境下保温0.5~3h;优选为每千克亚麻纤维用机械油10~20g、用NaOH 3~6g、洗涤剂2~8g,与10kg水搅拌调制成乳化液,将亚麻纤维浸渍其中,在80℃的环境下保温1h。 According to the preparation method described above, the oil agent in the described oiling step is mechanical oil, preferably spindle oil or white oil; 10-40g of mechanical oil, 1-8g of NaOH, and 2-10g of detergent are used for every kilogram of flax fiber. , mixed with 8-12kg of water to prepare an emulsion, soak the flax fiber in it, and keep it warm for 0.5-3h in an environment of 60-100°C; preferably use 10-20g of machine oil per kilogram of flax fiber, 3-6g of NaOH, Stir 2-8g of detergent with 10kg of water to make an emulsion, impregnate the flax fiber in it, and keep it warm at 80°C for 1 hour. the
根据前面所述的制备方法,所述的给油加湿步骤中采用植物油,优选为茶油或菜油;将植物油、NaOH、洗涤剂与水搅拌调制成乳化液,在软麻机麻条输出端均匀地将乳化液喷洒在亚麻纤维上,所述洗涤剂为常用洗涤剂;每千克亚麻纤维用植物油5~40g、用NaOH 1~10g、洗涤剂1~12g,水50~200g,优选为每千克亚麻纤维用植物油10~20g、用NaOH3~6g、洗涤剂2~8g,水70~150g。 According to the aforementioned preparation method, vegetable oil is used in the oiling and humidifying step, preferably camellia oil or rapeseed oil; vegetable oil, NaOH, detergent and water are stirred to form an emulsion, which is evenly distributed at the output end of the flax machine. The emulsion is sprayed on the flax fiber, and the detergent is a common detergent; per kilogram of flax fiber, vegetable oil 5-40g, NaOH 1-10g, detergent 1-12g, water 50-200g, preferably per kilogram Flax fibers use 10-20g of vegetable oil, 3-6g of NaOH, 2-8g of detergent, and 70-150g of water. the
根据前面所述的制备方法,所述的堆仓为温度20~60℃,时间15~60小时;优选为温度25~40℃,时间24~48小时。 According to the above-mentioned preparation method, the temperature of the stacking bin is 20-60° C., and the time is 15-60 hours; preferably, the temperature is 25-40° C., and the time is 24-48 hours. the
根据前面所述的制备方法,所述的机械开松步骤中刺辊与给棉板隔距采用0.10~7.50mm,优选为0.12~5.50mm。 According to the above-mentioned preparation method, in the mechanical opening step, the gap between the licker-in roller and the cotton feeding plate is 0.10-7.50 mm, preferably 0.12-5.50 mm. the
根据前面所述的制备方法,所述的机械开松步骤中梳棉机的给棉板要抬高1~5cm,优选为2~3cm。 According to the above-mentioned preparation method, in the mechanical opening step, the cotton feeding plate of the carding machine should be raised by 1-5 cm, preferably 2-3 cm. the
下面对本发明详细阐述: The present invention is described in detail below:
本发明提供的亚麻纤维强度为3.0~8.0cN/dtex、细度为1500~3500公支;优选为强度4.0~7.0cN/dtex、细度为1500~3000公支;更优选为强度4.5~6.5cN/dtex、细度为1800~2800公支;最优选为强度5.0~6.0cN/dtex、细度为2300~2700公支。 The flax fiber provided by the invention has a strength of 3.0 to 8.0 cN/dtex and a fineness of 1500 to 3500 branch; preferably a strength of 4.0 to 7.0 cN/dtex and a fineness of 1500 to 3000 branch; more preferably a strength of 4.5 to 6.5 cN/dtex, fineness 1800-2800 metric; most preferably strength 5.0-6.0cN/dtex, fineness 2300-2700 metric. the
本发明提供的亚麻纤维细度高,可以采用现有技术中比传统的亚麻湿纺更简单的棉纺、毛纺或苎麻纺设备进行干纺加工,纺制60公支以上的亚麻纯纺或混纺纱, 克服了湿法亚麻纱一般只能纺24~36公支左右的粗支纱的缺陷,可以用来制作高档织物,使得亚麻纤维的应用更加广泛。 The flax fiber provided by the invention has high fineness, and can be processed by dry spinning with cotton spinning, wool spinning or ramie spinning equipment which is simpler than traditional flax wet spinning in the prior art, and can be spun pure or blended flax with more than 60 public counts Yarn overcomes the defect that wet flax yarn can only be spun with a coarse count of about 24 to 36, and can be used to make high-grade fabrics, making flax fiber more widely used. the
本发明制备精细化亚麻纤维的工艺流程如下: The present invention prepares the technological process of refined flax fiber as follows:
亚麻打成麻→浸酸→水洗→氧化→打纤→给油→脱油水→软麻→给油加湿→堆仓→机械开松。 Flax is beaten into hemp→ pickling→washing→oxidation→fiberizing→oiling→deoiling→softening→oiling and humidification→stacking→mechanical opening. the
所述的氧化步骤为:通过双氧水与木质素反应形成易溶于稀碱液的氧化木质素,同时双氧水氧化纤维之间的胶质,使纤维之间的胶质膨松,降低纤维间的联系力,从而使纤维在经过机械作用后能分开。脱胶液的配制及氧化过程:每千克亚麻纤维用水8~12kg,即浴比为1∶8~1∶12。先在水中加入碳酸钠或碳酸钾、硅酸钠、尿素和渗透剂JFC(脂肪醇聚氧乙烯醚类化合物)等助剂,碳酸钠或碳酸钾溶液为弱碱,其碱性较柔和,加入适量碳酸钠或碳酸钾可以保证碱量足够去除胶质的情况下减轻碱对纤维的损伤,硅酸钠为双氧水稳定剂,尿素对纤维具有一定的蓬松作用,渗透剂可以增加化学药品对纤维的渗透作用,加入量为加入后每升水含碳酸钠2~6g、硅酸钠2~8g、尿素2~8g和渗透剂JFC1~4g,完全溶解后加入H2O2,H2O2加入量以纯H2O2计为加入后每升水含H2O23~12g。 The oxidation step is as follows: reacting hydrogen peroxide and lignin to form oxidized lignin that is easily soluble in dilute lye; at the same time, the hydrogen peroxide oxidizes the colloid between the fibers to make the colloid between the fibers bulky and reduce the connection between the fibers Force, so that the fibers can be separated after mechanical action. Preparation of degumming solution and oxidation process: 8-12kg of water per kilogram of flax fiber, that is, the bath ratio is 1:8-1:12. Add additives such as sodium carbonate or potassium carbonate, sodium silicate, urea and penetrant JFC (fatty alcohol polyoxyethylene ether compound) into the water first. The sodium carbonate or potassium carbonate solution is a weak base, and its alkalinity is soft. Appropriate amount of sodium carbonate or potassium carbonate can reduce the damage of alkali to fiber under the condition that the amount of alkali is enough to remove colloid. Sodium silicate is hydrogen peroxide stabilizer, urea has a certain fluffing effect on fiber, and penetrant can increase the effect of chemicals on fiber. Osmosis, the amount added is 2~6g of sodium carbonate, 2~8g of sodium silicate, 2~8g of urea and 1~4g of osmotic agent JFC per liter of water after addition. After completely dissolving, add H 2 O 2 . Calculated by pure H 2 O 2 , the content of H 2 O 2 per liter of water after addition is 3-12g.
其中可进一步优选每千克亚麻纤维用水10kg,每升水含碳酸钠或碳酸钾2~4g、硅酸钠3~5g、尿素3~5g、渗透剂JFC2g,H2O2加入量以纯H2O2计为加入后每升水含H2O23~8g。 Among them, 10kg of water per kilogram of flax fiber can be further preferred, and each liter of water contains 2-4g of sodium carbonate or potassium carbonate, 3-5g of sodium silicate, 3-5g of urea, 2g of penetrant JFC, and the amount of H 2 O 2 added is based on pure H 2 O 2 It is calculated as 3~8g of H 2 O 2 per liter of water after adding.
此外,所述的氧化步骤操作可以进一步优选为将亚麻放入氧化液中,从室温匀速升温至50~100℃,升温时间控制在20~60min,氧化反应时间为2.0~4.0小时;再优选为从室温匀速升温至70~90℃,升温时间控制在30~40min,氧化反应时间为1.0~3.0小时。 In addition, the operation of the oxidation step can be further preferably put flax in the oxidation solution, and the temperature is raised from room temperature to 50-100°C at a constant speed, the heating time is controlled at 20-60 minutes, and the oxidation reaction time is 2.0-4.0 hours; more preferably The temperature is raised from room temperature to 70-90°C at a constant speed, the heating time is controlled at 30-40 minutes, and the oxidation reaction time is 1.0-3.0 hours. the
所述的浸酸作用是初步去除亚麻打成麻纤维表皮的果胶,并去除亚麻纤维中的金属离子,金属离子会对氧化反应起到催化作用导致双氧水反应过快,从而对纤维过度氧化。酸的浓度、温度过高会造成纤维素的过度水解,酸的浓度、温度过低也不能达到去除果胶和纤维中金属离子的作用,本发明中浸酸过程可以参考现有技术的浸酸,然而为了进一步提高产品质量,优选浸酸过程中酸的浓度控制在1~3g/L,温度在35~70℃,浴比为1∶8~1∶12(即1公斤亚麻纤维加8~12公斤水),浸酸时间为30~80min;更优选为酸的浓度为1~2g/L,温度在40~50℃,浴比为1∶10,浸酸时间为40~60min。 The pickling effect is to preliminarily remove the pectin on the epidermis of the flax fiber and remove the metal ions in the flax fiber. The metal ion will catalyze the oxidation reaction and cause the hydrogen peroxide to react too quickly, thereby excessively oxidizing the fiber. Too high acid concentration and temperature will cause excessive hydrolysis of cellulose, and too low acid concentration and temperature can not achieve the effect of removing metal ions in pectin and fibers. In the present invention, the pickling process can refer to the prior art pickling However, in order to further improve product quality, the concentration of acid in the preferred pickling process is controlled at 1 to 3g/L, the temperature is at 35 to 70°C, and the bath ratio is 1:8 to 1:12 (that is, 1 kilogram of flax fiber plus 8 to 12 kg of water), the pickling time is 30-80min; more preferably, the acid concentration is 1-2g/L, the temperature is 40-50°C, the bath ratio is 1:10, and the pickling time is 40-60min. the
所述的酸为现有技术浸酸中可采用的任何酸,譬如有机类酸和无机类酸。其中可以优选的是盐酸、硫酸或草酸。 Described acid is any acid that can be adopted in pickling in the prior art, such as organic acid and inorganic acid. Of these, hydrochloric acid, sulfuric acid or oxalic acid may be preferred. the
其中水洗也可参考现有技术中任何水洗操作,本发明中优选为清水洗去亚麻纤维上残留的酸等杂质,使亚麻纤维的pH值在7左右,保持亚麻纤维的洁净。 Wherein water washing can also refer to any water washing operation in the prior art, preferably clean water washes away impurities such as acid remaining on the flax fiber among the present invention, makes the pH value of flax fiber be about 7, keeps the cleanliness of flax fiber. the
所述打纤也为现有技术任何打纤过程,通过打击,去除已从亚麻纤维中脱离,但仍粘附在亚麻纤维表面的杂质,一般打击2~5次。打击后进行水洗,其目的是洗去亚纤维上残留的氧化剂和胶质等,再次保持亚麻纤维的洁净并使亚麻纤维的pH值保持在7左右,水洗后脱水,利用工业离心脱水机将水洗后亚麻纤维上的大部分水分去除,其可以为现有技术任何水洗操作。 The fiber beating is also any fiber beating process in the prior art. The impurity that has been detached from the flax fiber but still adheres to the surface of the flax fiber is removed by beating, usually 2 to 5 times of beating. Washing after blowing, the purpose is to wash away the residual oxidants and colloids on the flax fiber, keep the flax fiber clean again and keep the pH value of the flax fiber at about 7, dehydrate after washing, and use an industrial centrifugal dehydrator to wash the flax fiber After most of the moisture on the flax fiber is removed, it can be any washing operation of the prior art. the
所述给油目的是防止残留在亚麻纤维表面的胶质经烘干后又将亚麻纤维粘结在一起;油剂的配制及给油过程:油剂为机械油,本领域技术人员通常知道亚麻纤维给油过程中应采用何种机械油,本领域技术人员对此无需作出创造性劳动,且本发明目的的实现也不被机械油种类所限。然而可以优选为锭子油或白油,机械油有很强的润滑作用,可以较有效地防止纤维重新粘结。给油操作可参考现有苎麻的给油过程,本发明优选油的用量:每千克亚麻纤维用机械油10~40g、用NaOH 1~8g、洗涤剂2~10g,与8~12kg水搅拌调制成乳化液,将亚麻纤维浸渍其中,在60~100℃的环境下保温0.5~3h。 The purpose of the oil supply is to prevent the colloid remaining on the surface of the flax fibers from bonding the flax fibers together after drying; the preparation and oil supply process of the oil agent: the oil agent is machine oil, and those skilled in the art generally know that the flax fiber What kind of mechanical oil should be used in the fiber oiling process, those skilled in the art do not need to do creative work on this, and the realization of the purpose of the present invention is not limited by the type of mechanical oil. However, it can be preferably spindle oil or white oil. Machine oil has a strong lubricating effect and can effectively prevent fibers from rebonding. The oil supply operation can refer to the existing ramie oil supply process. The preferred oil consumption of the present invention is: 10-40g of mechanical oil per kilogram of flax fiber, 1-8g of NaOH, 2-10g of detergent, and 8-12kg of water to stir and prepare Form an emulsified liquid, soak the flax fiber in it, and keep it warm for 0.5-3 hours under the environment of 60-100°C. the
所述给油还可进一步优选为每千克亚麻纤维用机械油10~20g、用NaOH 3~6g、洗涤剂2~8g,与10kg水搅拌调制成乳化液,将亚麻纤维浸渍其中,在80℃的环境下保温1h。 The oiling can further preferably be 10-20g of mechanical oil per kilogram of flax fiber, 3-6g of NaOH, 2-8g of detergent, stirred with 10kg of water to prepare an emulsion, and the flax fiber is soaked in it and heated at 80°C. Keep warm for 1h in the environment. the
所述脱油水为利用工业离心脱水机将给油后亚麻纤维上的大部分水分和浮油去除,然后烘干,本领域技术人员通常知晓这种脱油水的操作,无需再付出创造性劳动。 The deoiled water is to use an industrial centrifugal dehydrator to remove most of the moisture and slick oil on the oiled flax fiber, and then dry it. Those skilled in the art generally know the operation of this deoiled water, and no creative work is required. the
所述软麻为将烘干后的亚麻纤维经过多对罗拉的反复搓揉,使纤维柔软、松散,利于后道加工,其可参考现有苎麻的软麻操作。 The softening is that the dried flax fibers are repeatedly kneaded by multiple pairs of rollers to make the fibers soft and loose, which is beneficial to subsequent processing. It can refer to the existing ramie softening operation. the
由于烘干后纤维的水分太少,纤维毛糙且僵硬,为增加亚麻纤维表面的润滑性和柔软性,减少机械开松等后道加工中对亚麻纤维的损伤,要给亚麻添加一些油和水,即所述的给油加湿步骤。 Because the moisture of the fiber after drying is too little, the fiber is rough and stiff, in order to increase the lubricity and softness of the surface of the flax fiber, and reduce the damage to the flax fiber in the subsequent processing such as mechanical opening, some oil and water should be added to the flax , namely the described step of humidifying the oil. the
给油加湿亦可参考现有的亚麻给油加湿操作,即本领域技术人员通常知晓所述的给油加湿所采用的油的种类,且本发明目的是实现不受油种类所限。然而为进一 步提高亚麻纤维质量,本发明优选为:油一般采用植物油,因其具有一定的粘性,可以适当提高纤维之间的抱合力。油的用量:每千克亚麻纤维用植物油5~40g、用NaOH 1~10g、洗涤剂1~12g,与50~200g(视回潮率的需要)的水搅拌调制成乳化液,在软麻工序上均匀地将乳化液喷洒在亚麻纤维上(同现有的苎麻软麻操作一样)。 Oil humidification can also refer to the existing linseed oil humidification operation, that is, those skilled in the art usually know the type of oil used in the oil humidification, and the purpose of the present invention is not limited by the type of oil. Yet for further improving flax fiber quality, the present invention is preferably: oil generally adopts vegetable oil, because it has certain viscosity, can suitably improve the cohesive force between the fibers. The amount of oil used: 5-40g of vegetable oil per kilogram of flax fiber, 1-10g of NaOH, 1-12g of detergent, and 50-200g of water (depending on the need for moisture regain) are stirred to make an emulsion, which is used in the softening process Evenly spray the emulsion on the flax fiber (the same as the existing ramie soft hemp operation). the
所述给油加湿亦可再优选为每千克亚麻纤维用植物油10~20g、用NaOH3~6g、洗涤剂2~8g,水70~150g。 The oil humidification can also preferably use 10-20 g of vegetable oil per kilogram of flax fiber, 3-6 g of NaOH, 2-8 g of detergent, and 70-150 g of water. the
所述堆仓是为了使所加的油、水能均匀地渗透到亚麻纤维内部,其可以为现有技术任何堆仓操作,本发明优选为温度20~60℃,时间15~60小时;更优选为温度25~40℃,时间24~48小时。 The stacking is to make the added oil and water permeate into the inside of the flax fiber evenly, it can be any stacking operation in the prior art, and the present invention preferably has a temperature of 20-60°C and a time of 15-60 hours; more Preferably, the temperature is 25-40° C. and the time is 24-48 hours. the
所述机械开松是将堆仓后的亚麻纤维喂入开松机械,使亚麻纤维经过初步的松散分解后,再将其喂入梳棉机进行细致的开松、分劈。具体操作可参考现有技术任何机械开松的操作,本发明为了进一步减少开松梳理时对亚麻纤维的损伤,保证纤维长度,优选刺辊与给棉板隔距采用0.10~7.50mm,更优选为0.12~5.50mm。 The mechanical opening is to feed the heaped flax fibers into the opening machine, so that the flax fibers are preliminarily loosened and decomposed, and then fed into the carding machine for careful opening and splitting. The specific operation can refer to any mechanical opening operation in the prior art. In order to further reduce the damage to the flax fiber during opening and carding in the present invention and ensure the fiber length, the preferred spacing between the licker-in roller and the cotton feeding plate is 0.10-7.50 mm, more preferably 0.12 to 5.50mm. the
此外,梳棉机的给棉板还可进一步抬高1~5cm以增加分梳工艺长度,优选为抬高2~3cm。这种梳棉机可参见现有技术的梳棉机,本发明中仅仅是将给棉板抬高。也就是说,本领域技术人员均知道这种具有给棉板的梳棉机的结构,本领域技术人员仅需要将所述的给棉板太高1~5cm。 In addition, the feeding plate of the carding machine can be further raised by 1-5 cm to increase the length of the carding process, preferably by 2-3 cm. This carding machine can be referred to the carding machine of prior art, and in the present invention, only cotton feeding plate is raised. That is to say, those skilled in the art know the structure of the carding machine with the cotton feeding plate, and those skilled in the art only need to make the cotton feeding plate too high by 1-5 cm. the
本发明公开制备的精细化亚麻纤维,能利用现有的毛纺、苎麻纺和棉纺的纺纱工艺设备完成干纺加工,纺制60公支以上的亚麻纯纺或混纺纱,不仅大大缩短了传统亚麻湿法纺纱的工序,还克服了湿纺亚麻纱只能纺粗支(主要在24~36公支)纱,且纱僵硬,难以针织应用的缺陷。本方法加工出的亚麻及其混纺纱,可用作针织面料、高档服装和装饰用织物,使亚麻纤维的应用更为广泛。 The refined flax fiber prepared by the present invention can utilize the existing spinning process equipment of wool spinning, ramie spinning and cotton spinning to complete the dry spinning process, and spin flax pure spinning or blended yarn with more than 60 public counts, which not only greatly shortens the The traditional linen wet-spinning process also overcomes the defect that wet-spun linen yarn can only be spun with coarse counts (mainly 24-36 public counts), and the yarn is stiff, which is difficult for knitting applications. The flax and its blended yarn processed by the method can be used as knitted fabrics, high-grade clothing and decorative fabrics, so that the flax fibers can be more widely used. the
与现有技术相比,本发明的优点如下: Compared with prior art, advantage of the present invention is as follows:
1、本发明公开的化学处理过程中主要使用的药品为双氧水,碱用量较少,仅起辅助作用,所以处理后的废水pH值在7~8,环境污染大大减少; 1. The medicine mainly used in the chemical treatment process disclosed by the present invention is hydrogen peroxide, and the amount of alkali is less, which only plays an auxiliary role, so the pH value of the treated wastewater is 7-8, and the environmental pollution is greatly reduced;
2、本发明公开制备的精细化亚麻纤维,大大改善了亚麻纤维的可纺性(长度和细度等),使其能利用现有的棉纺或毛纺设备完成干纺加工,其棉纺流程为:开清→梳棉→预并→精梳→并条→粗纱→细纱→后加工;其毛纺或苎麻纺的流程是:梳理→并条→精梳→针梳→粗纱→细纱→后加工。它们与常规的亚麻湿纺工序相比,大大缩短了纺纱流程,并能纺制60公支以上的亚麻纯纺或混纺纱,克服了传统湿法亚 麻纱只能纺粗支(主要在24-36公支)纱,且纱僵硬,难以针织应用的缺陷,满足了纺高支纱和制成高档的服装和装饰用织物的需求。 2. The fine flax fiber prepared by the present invention greatly improves the spinnability (length and fineness, etc.) of the flax fiber, so that it can utilize existing cotton spinning or wool spinning equipment to complete dry spinning processing, and its cotton spinning process is: Blowroom→carding→pre-combing→combing→drawing→roving→spinning→post-processing; the process of wool spinning or ramie spinning is: carding→drawing→combing→pinning→roving→spinning→post-processing. Compared with the conventional flax wet spinning process, they greatly shorten the spinning process, and can spin pure flax or blended yarns of more than 60 public counts, overcoming the fact that traditional wet linen yarns can only be spun with coarse counts (mainly in 24-36 public count) yarn, and the yarn is stiff and difficult to be used in knitting, which meets the needs of spinning high-count yarn and making high-grade clothing and decorative fabrics. the
3、本发明所制备的亚麻纤维细度、强度高,进一步扩大了亚麻纤维的使用领域。 3. The flax fiber prepared by the present invention has high fineness and high strength, which further expands the field of use of the flax fiber. the
具体实施方式Detailed ways
下面的实施例将对本发明作更具体的解释,但本发明并不仅仅局限于这些实施例,同样这些实施例也不以任何方式限制本发明。 The following examples will explain the present invention more specifically, but the present invention is not limited to these examples, nor are these examples limiting the present invention in any way. the
实施例1: Example 1:
将亚麻打成麻放入浸酸池中,每公斤亚麻用水10公斤(浴比1∶10),加入硫酸,使硫酸浓度为1g/L。将溶液温度升至40℃,保温40min后取出用清水对亚麻纤维进行清洗,使亚麻纤维的pH值达到7左右;将清洗后的亚麻纤维放入氧化液中,浴比采用1∶10,氧化液中双氧水(按纯按纯H2O2算)含量为3g/L,硅酸钠含量3g/L,碳酸钾含量2g/L,尿素含量3g/L,JFC含量2g/L。将氧化液的温度由常温匀速升至70℃,升温时间控制在30min,温度到达后让氧化液保温2h;用木槌对氧化后的亚麻纤维进行敲打,打击2次;用清水对敲打后的亚麻纤维进行清洗,洗去残留在纤维表面的药品和杂质。利用离心脱水机将亚麻纤维脱水,脱水后将亚麻纤维浸泡的乳化油中,每公斤亚麻纤维用锭子油10g,NaOH3g、洗涤剂2g,与10kg水搅拌形成乳化液,将亚麻纤维浸渍其中,在80℃的环境下保温1h。将给油后的纤维脱水,经烘干机烘干。烘干后的亚麻纤维经过软麻机加工,并喷上乳化液,其成分为(每公斤亚麻):茶油10g,NaOH3g、洗涤剂2g,150g的水搅拌调制成乳化液,然后放入温度为27℃的仓中24h。利用带有针齿的开松机械对堆仓后的亚麻纤维进行初步开松后,再将其喂入梳棉机中进行进一步的开松、分劈,梳棉机给棉板抬高2cm,刺辊与给棉板隔距采用5.5mm。 Beat flax into hemp and put it in the pickling pool, add 10 kg of water per kg of flax (bath ratio 1:10), add sulfuric acid to make the concentration of sulfuric acid 1g/L. Raise the temperature of the solution to 40°C, keep it warm for 40 minutes, take it out and wash the flax fiber with clean water, so that the pH value of the flax fiber reaches about 7; put the washed flax fiber into the oxidation solution, the bath ratio is 1:10, and oxidize The content of hydrogen peroxide (calculated as pure H 2 O 2 ) in the liquid is 3g/L, the content of sodium silicate is 3g/L, the content of potassium carbonate is 2g/L, the content of urea is 3g/L, and the content of JFC is 2g/L. Raise the temperature of the oxidizing solution from room temperature to 70°C at a constant speed, and control the heating time at 30 minutes. After reaching the temperature, let the oxidizing solution keep warm for 2 hours; beat the oxidized flax fiber twice with a wooden mallet; The flax fiber is cleaned to remove the medicines and impurities remaining on the surface of the fiber. Use a centrifugal dehydrator to dehydrate the flax fiber. After dehydration, in the emulsified oil soaked in the flax fiber, 10g of spindle oil, 3g of NaOH, and 2g of detergent per kilogram of flax fiber are stirred with 10kg of water to form an emulsion, and the flax fiber is soaked in it. Incubate at 80°C for 1 hour. The oiled fibers are dehydrated and dried by a dryer. The dried flax fibers are processed by a flax softening machine and sprayed with an emulsion. The ingredients are (per kilogram of flax): 10g of tea oil, 3g of NaOH, 2g of detergent, and 150g of water. 24h in a warehouse at 27°C. Use the opening machine with pin teeth to initially open the flax fiber after stacking, and then feed it into the carding machine for further opening and splitting. The carding machine raises the cotton board by 2cm, The gap between the licker-in roller and the cotton feeding board is 5.5mm.
采用以上工艺制备的精细化亚麻纤维的主要性能指标如下: The main performance indicators of the refined flax fiber prepared by the above process are as follows:
表1、实施例1制备的亚麻纤维主要性能指标 Table 1, the flax fiber main performance index that embodiment 1 prepares
实施例2: Example 2:
将亚麻打成麻放入浸酸池中,每公斤亚麻用水10公斤(浴比1∶10),加入硫酸,使硫酸浓度为2g/L。将溶液温度升至50℃,保温45min后取出用清水对亚麻纤维进行清洗,使亚麻纤维的pH值达到7左右;将清洗后的亚麻纤维放入氧化液中,浴比采用1∶10,氧化液中双氧水(按纯按纯H2O2算)含量为4g/L,硅酸钠含量4g/L,碳酸钠含量3g/L,尿素含量4g/L,JFC含量2g/L。将氧化液的温度由常温匀速升至80℃,升温时间控制在32min,温度到达后让氧化液保温2.2h;用木槌对氧化后的亚麻纤维进行敲打,打击2次;用清水对敲打后的亚麻纤维进行清洗,洗去残留在纤维表面的药品和杂质。利用离心脱水机将亚麻纤维脱水,脱水后将亚麻纤维浸泡的乳化油中,每公斤亚麻纤维用锭子油12g,NaOH4g、洗涤剂3g,与水10kg搅拌形成乳化液,将亚麻纤维浸渍其中,在80℃的环境下保温1h。将给油后的纤维脱水,经烘干机烘干。烘干后的亚麻纤维经过软麻机加工,并喷上乳化液,其成分为(每公斤亚麻):菜油12g,NaOH3.5g、洗涤剂8g,120g的水搅拌调制成乳化液,然后放入温度为25℃的仓中30h。利用带有针齿的开松机械对堆仓后的亚麻纤维进行初步开松后,再将其喂入梳棉机中进行进一步的开松、分劈,梳棉机给棉板抬高2.5cm,刺辊与给棉板隔距采用0.12mm。 Beat flax into hemp and put it in the pickling pool, add 10 kg of water per kg of flax (bath ratio 1:10), add sulfuric acid to make the concentration of sulfuric acid 2g/L. Raise the temperature of the solution to 50°C, keep it warm for 45 minutes, take it out and wash the flax fiber with clean water, so that the pH value of the flax fiber reaches about 7; put the washed flax fiber into the oxidation solution, the bath ratio is 1:10, The content of hydrogen peroxide (calculated as pure H 2 O 2 ) in the liquid is 4g/L, sodium silicate content 4g/L, sodium carbonate content 3g/L, urea content 4g/L, JFC content 2g/L. Raise the temperature of the oxidizing solution from normal temperature to 80°C at a constant speed, and control the heating time at 32 minutes. After the temperature reaches, let the oxidizing solution keep warm for 2.2 hours; beat the oxidized flax fiber with a wooden mallet twice; The flax fiber is cleaned to wash away the medicines and impurities remaining on the surface of the fiber. Use a centrifugal dehydrator to dehydrate the flax fiber. After dehydration, in the emulsified oil soaked in the flax fiber, use 12g of spindle oil, 4g of NaOH, and 3g of detergent per kilogram of flax fiber, stir with 10kg of water to form an emulsion, and soak the flax fiber in it. Incubate at 80°C for 1 hour. The oiled fibers are dehydrated and dried by a dryer. The dried flax fibers are processed by a flax softening machine and sprayed with an emulsion. The ingredients are (per kilogram of flax): 12g of rapeseed oil, 3.5g of NaOH, 8g of detergent, and 120g of water. 30h in a warehouse at a temperature of 25°C. Use the opening machine with pin teeth to initially open the flax fiber after stacking, and then feed it into the carding machine for further opening and splitting. The carding machine raises the cotton board by 2.5cm , The gap between the licker-in roller and the cotton feeding board is 0.12mm.
采用以上工艺制备的精细化亚麻纤维的主要性能指标如下: The main performance indicators of the refined flax fiber prepared by the above process are as follows:
表2、实施例2制备的亚麻纤维主要性能指标 The flax fiber main performance index prepared by table 2, embodiment 2
实施例3: Example 3:
将亚麻打成麻放入浸酸池中,每公斤亚麻用水10公斤(浴比1∶10),加入硫酸,使硫酸浓度为1.5g/L。将溶液温度升至42℃,保温50min后取出用清水对亚麻纤维进行清洗,使亚麻纤维的pH值达到7左右;将清洗后的亚麻纤维放入氧化液中,浴比采用1∶10,氧化液中双氧水(按纯按纯H2O2算)含量为5g/L,碳酸钠含量4g/L,硅酸钠含量5g/L,尿素含量5g/L,JFC含量2g/L。将氧化液的温度由常温匀速升至90℃,升温时间控制在34min,温度到达后让氧化液保温2.4h;用木槌对氧化后的亚麻纤维进行敲打,打击5次;用清水对敲打后的亚麻纤维进行清洗,洗去残留在纤维表面的药品和杂质。利用离心脱水机将亚麻纤维脱水,脱水后将亚麻纤维浸泡的乳化油中,每公斤亚麻纤维用锭子油15g,NaOH5g、洗涤剂4g,与水10kg搅拌形 成乳化液,将亚麻纤维浸渍其中,在80℃的环境下保温1h。将给油后的纤维脱水,再脱去油水,经烘干机烘干。烘干后的亚麻纤维经过软麻机加工,并喷上乳化液,其成分为(每公斤亚麻):菜油14g,NaOH4g、洗涤剂7g,100g的水搅拌调制成乳化液,然后放入温度为38℃的仓中43h;利用带针齿的开松机械对堆仓后的亚麻纤维进行初步开松,再将开松后的纤维喂入梳棉机中进一步细致的开松、分劈,梳棉机给棉板抬高3cm,刺辊与给棉板隔距采用4.4mm。 Beat flax into hemp and put it in the pickling pool, add 10 kg of water per kg of flax (bath ratio 1:10), add sulfuric acid to make the concentration of sulfuric acid 1.5g/L. Raise the temperature of the solution to 42°C, keep it warm for 50 minutes, take it out and wash the flax fiber with clean water, so that the pH value of the flax fiber reaches about 7; put the washed flax fiber into the oxidation solution, the bath ratio is 1:10, and oxidize The content of hydrogen peroxide (calculated as pure H 2 O 2 ) in the liquid is 5g/L, the content of sodium carbonate is 4g/L, the content of sodium silicate is 5g/L, the content of urea is 5g/L, and the content of JFC is 2g/L. Raise the temperature of the oxidizing solution from room temperature to 90°C at a constant speed, and control the heating time at 34 minutes. After reaching the temperature, let the oxidizing solution keep warm for 2.4 hours; beat the oxidized flax fibers with a wooden mallet for 5 times; The flax fiber is cleaned to wash away the medicines and impurities remaining on the surface of the fiber. Use a centrifugal dehydrator to dehydrate the flax fiber. After dehydration, in the emulsified oil soaked in the flax fiber, 15g of spindle oil, 5g of NaOH, and 4g of detergent are used for each kilogram of flax fiber, and stirred with 10kg of water to form an emulsion, and the flax fiber is soaked in it. Incubate at 80°C for 1 hour. The oiled fibers are dehydrated, then the oil and water are removed, and then dried by a dryer. The dried flax fiber is processed by a flax softening machine and sprayed with an emulsion. Its composition is (per kilogram of flax): 14g of rapeseed oil, 4g of NaOH, 7g of detergent, and 100g of water are stirred to form an emulsion, and then put into a temperature of 43 hours in the bin at 38°C; use the opening machine with needle teeth to preliminarily open the flax fibers after stacking, and then feed the opened fibers into the carding machine for further detailed opening, splitting, and carding. The feeding board of the cotton machine is raised by 3cm, and the distance between the licker-in roller and the feeding board is 4.4mm.
采用以上工艺制备的精细化亚麻纤维的主要性能指标如下: The main performance indicators of the refined flax fiber prepared by the above process are as follows:
表3、实施例3制备的亚麻纤维主要性能指标 Table 3, the flax fiber main performance index that embodiment 3 prepares
实施例4: Example 4:
将亚麻打成麻放入浸酸池中,每公斤亚麻用水10公斤(浴比1∶10),加入硫酸,使硫酸浓度为1.2g/L。将溶液温度升至45℃,保温55min后取出用清水对亚麻纤维进行清洗,使亚麻纤维的pH值达到7左右;将清洗后的亚麻纤维放入氧化液中,浴比采用1∶10,氧化液中双氧水(按纯按纯H2O2算)含量为6g/L,硅酸钠含量3.5g/L,碳酸钾含量2g/L,尿素含量3.5g/L,JFC含量2g/L。将氧化液的温度由常温匀速升至75℃,升温时间控制在35min,温度到达后让氧化液保温2.6h;用木槌对氧化后的亚麻纤维进行敲打,打击5次;用清水对敲打后的亚麻纤维进行清洗,洗去残留在纤维表面的药品和杂质。利用离心脱水机将亚麻纤维脱水,脱水后将亚麻纤维浸泡的乳化油中,每公斤亚麻纤维用锭子油17g,NaOH3.5g、洗涤剂5g,与水10kg搅拌形成乳化液,将亚麻纤维浸渍其中,在80℃的环境下保温1h。将给油后的纤维脱水,经烘干机烘干。烘干后的亚麻纤维经过软麻机加工,并喷上乳化液,其成分为(每公斤亚麻):茶油16g,NaOH4.5g、洗涤剂6g,70g的水搅拌调制成乳化液,然后放入温度为35℃的仓中48h。利用带有针齿的开松机械对堆仓后的亚麻纤维进行初步开松后,再将其喂入梳棉机中进行进一步的开松、分劈,梳棉机给棉板抬高2.2cm,刺辊与给棉板隔距采用3.5mm。 Beat flax into hemp and put it in the pickling pool, add 10 kg of water per kg of flax (bath ratio 1:10), add sulfuric acid to make the concentration of sulfuric acid 1.2g/L. Raise the temperature of the solution to 45°C, keep it warm for 55 minutes, take it out and wash the flax fiber with clean water, so that the pH value of the flax fiber reaches about 7; put the washed flax fiber into the oxidation solution, the bath ratio is 1:10, and oxidize The content of hydrogen peroxide ( calculated as pure H2O2 ) in the liquid is 6g/L, the content of sodium silicate is 3.5g/L, the content of potassium carbonate is 2g/L, the content of urea is 3.5g/L, and the content of JFC is 2g/L. Raise the temperature of the oxidizing solution from normal temperature to 75°C at a constant speed, and control the heating time at 35 minutes. After the temperature reaches, let the oxidizing solution keep warm for 2.6 hours; beat the oxidized flax fibers with a wooden mallet for 5 times; The flax fiber is cleaned to wash away the medicines and impurities remaining on the surface of the fiber. Use a centrifugal dehydrator to dehydrate the flax fiber. After dehydration, soak the flax fiber in the emulsified oil. For each kilogram of flax fiber, use 17g of spindle oil, 3.5g of NaOH, and 5g of detergent. Stir with 10kg of water to form an emulsion, and impregnate the flax fiber in it. , kept at 80°C for 1h. The oiled fibers are dehydrated and dried by a dryer. The dried flax fiber is processed by a softening machine and sprayed with an emulsion. The composition is (per kilogram of flax): 16g of tea oil, 4.5g of NaOH, 6g of detergent, and 70g of water are stirred to form an emulsion, and then put Put it into a warehouse at a temperature of 35°C for 48 hours. Use the opening machine with needle teeth to initially open the flax fiber after stacking, and then feed it into the carding machine for further opening and splitting. The carding machine raises the cotton board by 2.2cm , The gap between the licker-in roller and the cotton feeding board is 3.5mm.
采用以上工艺制备的精细化亚麻纤维的主要性能指标如下: The main performance indicators of the refined flax fiber prepared by the above process are as follows:
表4、实施例4制备的亚麻纤维主要性能指标 The flax fiber main performance index prepared by table 4, embodiment 4
实施例5: Embodiment 5:
将亚麻打成麻放入浸酸池中,每公斤亚麻用水10公斤(浴比1∶10),加入盐酸,盐酸浓度为1.8g/L。将溶液温度升至48℃,保温58min后取出用清水对亚麻纤维进行清洗,使亚麻纤维的pH值达到7左右;将清洗后的亚麻纤维放入氧化液中,浴比采用1∶10,氧化液中双氧水(按纯按纯H2O2算)含量为7g/L,硅酸钠含量4.5g/L,碳酸钾含量3g/L,尿素含量4.5g/L,JFC含量2g/L。将氧化液的温度由常温匀速升至85℃,升温时间控制在37min,温度到达后让氧化液保温2.8h;用木槌对氧化后的亚麻纤维进行敲打,打击5次;用清水对敲打后的亚麻纤维进行清洗,洗去残留在纤维表面的药品和杂质。利用离心脱水机将亚麻纤维脱水,脱水后将亚麻纤维浸泡的乳化油中,每公斤亚麻纤维用锭子油19g,NaOH4.5g、洗涤剂6g,与水10kg搅拌形成乳化液,将亚麻纤维浸渍其中,在80℃的环境下保温1h。将给油后的纤维脱水,经烘干机烘干。烘干后的亚麻纤维经过软麻机加工,并喷上乳化液,其成分为(每公斤亚麻):菜油18g,NaOH5g、洗涤剂5g,80g的水搅拌调制成乳化液,然后放入温度为40℃的仓中38h。利用带有针齿的开松机械对堆仓后的亚麻纤维进行初步开松后,再将其喂入梳棉机中进行进一步的开松、分劈,梳棉机给棉板抬高2.7cm,刺辊与给棉板隔距采用2.7mm。 Beat the flax into hemp and put it in the pickling pool, add 10 kg of water per kg of flax (bath ratio 1:10), add hydrochloric acid, the concentration of hydrochloric acid is 1.8g/L. Raise the temperature of the solution to 48°C, keep it warm for 58 minutes, take it out and wash the flax fiber with clean water, so that the pH value of the flax fiber reaches about 7; put the washed flax fiber into the oxidation solution, the bath ratio is 1:10, and oxidize The content of hydrogen peroxide (calculated as pure H 2 O 2 ) in the liquid is 7g/L, the content of sodium silicate is 4.5g/L, the content of potassium carbonate is 3g/L, the content of urea is 4.5g/L, and the content of JFC is 2g/L. Raise the temperature of the oxidizing solution from normal temperature to 85°C at a constant speed, and control the heating time at 37 minutes. After the temperature reaches, let the oxidizing solution keep warm for 2.8 hours; beat the oxidized flax fiber with a wooden mallet for 5 times; The flax fiber is cleaned to wash away the medicines and impurities remaining on the surface of the fiber. Use a centrifugal dehydrator to dehydrate the flax fiber. After dehydration, soak the flax fiber in the emulsified oil. For each kilogram of flax fiber, use 19g of spindle oil, 4.5g of NaOH, and 6g of detergent. Stir with 10kg of water to form an emulsion, and soak the flax fiber in it , kept at 80°C for 1h. The oiled fibers are dehydrated and dried by a dryer. The flax fibers after drying are processed by a flax softening machine and sprayed with an emulsion. The composition is (per kilogram of flax): 18g of rapeseed oil, 5g of NaOH, 5g of detergent, and 80g of water are stirred to form an emulsion, and then put into the emulsion at a temperature of 38h in a warehouse at 40°C. Use the opening machine with pin teeth to initially open the flax fiber after stacking, and then feed it into the carding machine for further opening and splitting. The carding machine raises the cotton board by 2.7cm , The gap between the licker-in roller and the cotton feeding board is 2.7mm.
采用以上工艺制备的精细化亚麻纤维的主要性能指标如下: The main performance indicators of the refined flax fiber prepared by the above process are as follows:
表5、实施例5制备的亚麻纤维主要性能指标 Table 5, main performance index of the flax fiber prepared by embodiment 5
实施例6: Embodiment 6:
将亚麻打成麻放入浸酸池中,每公斤亚麻用水10公斤(浴比1∶10),加入盐酸,盐酸浓度为2.1g/L。将溶液温度升至38℃,保温60min后取出用清水对亚麻纤维进行清洗,使亚麻纤维的pH值达到7左右;将清洗后的亚麻纤维放入氧化液中,浴比采用1∶10,氧化液中双氧水(按纯按纯H2O2算)含量为8g/L,硅酸钠含量5.0g/L,碳酸钾含量4g/L,尿素含量5.0g/L,JFC含量2g/L。将氧化液的温度由常温匀速升 至90℃,升温时间控制在40min,温度到达后让氧化液保温3h;用木槌对氧化后的亚麻纤维进行敲打,打击5次;用清水对敲打后的亚麻纤维进行清洗,洗去残留在纤维表面的药品和杂质。利用离心脱水机将亚麻纤维脱水,脱水后将亚麻纤维浸泡的乳化油中,每公斤亚麻纤维用锭子油20g,NaOH6g、洗涤剂8g,与水10kg搅拌形成乳化液,将亚麻纤维浸渍其中,在80℃的环境下保温1h。将给油后的纤维脱水,经烘干机烘干。烘干后的亚麻纤维经过软麻机加工,并喷上乳化液,其成分为(每公斤亚麻):茶油20g,NaOH6g、洗涤剂4g,90g的水搅拌调制成乳化液,然后放入温度为33℃的仓中34h。利用带有针齿的开松机械对堆仓后的亚麻纤维进行初步开松后,再将其喂入梳棉机中进行进一步的开松、分劈,梳棉机给棉板抬高2.9cm,刺辊与给棉板隔距采用1.5mm。 Beat the flax into hemp and put it in the pickling pool, add 10 kg of water per kg of flax (bath ratio 1:10), add hydrochloric acid, the concentration of hydrochloric acid is 2.1g/L. Raise the temperature of the solution to 38°C, keep it warm for 60 minutes, take it out and wash the flax fiber with clean water, so that the pH value of the flax fiber reaches about 7; put the washed flax fiber into the oxidation solution, the bath ratio is 1:10, and oxidize The content of hydrogen peroxide ( calculated as pure H2O2 ) in the solution is 8g/L, the content of sodium silicate is 5.0g/L, the content of potassium carbonate is 4g/L, the content of urea is 5.0g/L, and the content of JFC is 2g/L. Raise the temperature of the oxidizing solution from normal temperature to 90°C at a constant speed, and control the heating time at 40 minutes. After reaching the temperature, let the oxidizing solution keep warm for 3 hours; beat the oxidized flax fiber with a wooden mallet for 5 times; The flax fiber is cleaned to remove the medicines and impurities remaining on the surface of the fiber. Use a centrifugal dehydrator to dehydrate the flax fiber. After dehydration, in the emulsified oil soaked in the flax fiber, use 20g of spindle oil, 6g of NaOH, and 8g of detergent per kilogram of flax fiber, stir with 10kg of water to form an emulsion, and soak the flax fiber in it. Incubate at 80°C for 1 hour. The oiled fibers are dehydrated and dried by a dryer. The dried flax fibers are processed by a flax softening machine and sprayed with an emulsion. The ingredients are (per kilogram of flax): 20g of tea oil, 6g of NaOH, 4g of detergent, and 90g of water are stirred to form an emulsion, and then placed in a temperature 34h in a warehouse at 33°C. Use the opening machine with pin teeth to initially open the flax fiber after stacking, and then feed it into the carding machine for further opening and splitting. The carding machine raises the cotton board by 2.9cm , The gap between the licker-in roller and the cotton feeding board is 1.5mm.
采用以上工艺制备的精细化亚麻纤维的主要性能指标如下: The main performance indicators of the refined flax fiber prepared by the above process are as follows:
表6、实施例6制备的亚麻纤维主要性能指标 Table 6, the flax fiber main performance index that embodiment 6 prepares
实施例7: Embodiment 7:
将亚麻打成麻放入浸酸池中,每公斤亚麻用水8公斤(浴比1∶8),加入硫酸,硫酸浓度为2.3g/L。将溶液温度升至35℃,保温30min后取出用清水对亚麻纤维进行清洗,使亚麻纤维的pH值达到7左右;将清洗后的亚麻纤维放入氧化液中,浴比采用1∶8,氧化液中双氧水(按纯按纯H2O2算)含量为9g/L,硅酸钠含量2g/L,碳酸钠含量5g/L,尿素含量6g/L,JFC含量1g/L。将氧化液的温度由常温匀速升至93℃,升温时间控制在20min,温度到达后让氧化液保温3.2h;用木槌对氧化后的亚麻纤维进行敲打,打击5次;用清水对敲打后的亚麻纤维进行清洗,洗去残留在纤维表面的药品和杂质。利用离心脱水机将亚麻纤维脱水,脱水后将亚麻纤维浸泡的乳化油中,每公斤亚麻纤维用白油23g,NaOH1g、洗涤剂9g,与水8kg搅拌形成乳化液,将亚麻纤维浸渍其中,在60℃的环境下保温3h。将给油后的纤维脱水,经烘干机烘干。烘干后的亚麻纤维经过软麻机加工,并喷上乳化液,其成分为(每公斤亚麻):植物油5g,NaOH1g、洗涤剂1g,50g的水搅拌调制成乳化液,然后放入温度为20℃的仓中60h。利用带有针齿的开松机械对堆仓后的亚麻纤维进行初步开松后,再将其喂 入梳棉机中进行进一步的开松、分劈,梳棉机给棉板抬高1.0cm,刺辊与给棉板隔距采用7.0mm。 Beat the flax into hemp and put it in the pickling pool, add 8 kg of water per kg of flax (bath ratio 1:8), add sulfuric acid, the concentration of sulfuric acid is 2.3g/L. Raise the temperature of the solution to 35°C, keep it warm for 30 minutes, take it out and wash the flax fiber with clean water, so that the pH value of the flax fiber reaches about 7; put the washed flax fiber into the oxidation solution, the bath ratio is 1:8, and oxidize The content of hydrogen peroxide ( calculated as pure H2O2 ) in the liquid is 9g/L, the content of sodium silicate is 2g/L, the content of sodium carbonate is 5g/L, the content of urea is 6g/L, and the content of JFC is 1g/L. Raise the temperature of the oxidizing solution from room temperature to 93°C at a constant speed, and control the heating time at 20 minutes. After reaching the temperature, let the oxidizing solution keep warm for 3.2 hours; beat the oxidized flax fibers with a wooden mallet for 5 times; The flax fiber is cleaned to wash away the medicines and impurities remaining on the surface of the fiber. Use a centrifugal dehydrator to dehydrate the flax fiber. After dehydration, in the emulsified oil soaked in the flax fiber, use 23g of white oil, 1g of NaOH, and 9g of detergent per kilogram of flax fiber, stir with 8kg of water to form an emulsion, and soak the flax fiber in it. Incubate at 60°C for 3 hours. The oiled fibers are dehydrated and dried by a dryer. The dried flax fiber is processed by a flax softening machine and sprayed with an emulsion. Its composition is (per kilogram of flax): 5g of vegetable oil, 1g of NaOH, 1g of detergent, and 50g of water are stirred to form an emulsion, and then put into the emulsion at a temperature of 60h in a warehouse at 20°C. Use the opening machine with pin teeth to initially open the flax fiber after stacking, and then feed it into the carding machine for further opening and splitting. The carding machine raises the cotton board by 1.0cm , The gap between the licker-in roller and the cotton feeding board is 7.0mm.
采用以上工艺制备的精细化亚麻纤维的主要性能指标如下: The main performance indicators of the refined flax fiber prepared by the above process are as follows:
表7、实施例7制备的亚麻纤维主要性能指标 Table 7, main performance index of flax fiber prepared by embodiment 7
实施例8: Embodiment 8:
将亚麻打成麻放入浸酸池中,每公斤亚麻用水9公斤(浴比1∶9),加入草酸,草酸浓度为2.4g/L。将溶液温度升至70℃,保温70min后取出用清水对亚麻纤维进行清洗,使亚麻纤维的pH值达到7左右;将清洗后的亚麻纤维放入氧化液中,浴比采用1∶9,氧化液中双氧水(按纯按纯H2O2算)含量为10g/L,硅酸钠含量6g/L,碳酸钠含量6g/L,尿素含量7g/L,JFC含量3g/L。将氧化液的温度由常温匀速升至95℃,升温时间控制在45min,温度到达后让氧化液保温3.5h;用木槌对氧化后的亚麻纤维进行敲打,打击5次;用清水对敲打后的亚麻纤维进行清洗,洗去残留在纤维表面的药品和杂质。利用离心脱水机将亚麻纤维脱水,脱水后将亚麻纤维浸泡的乳化油中,每公斤亚麻纤维用白油27g,NaOH2g、洗涤剂9.5g,与水9kg搅拌形成乳化液,将亚麻纤维浸渍其中,在70℃的环境下保温2h。将给油后的纤维脱水,经烘干机烘干。烘干后的亚麻纤维经过软麻机加工,并喷上乳化液,其成分为(每公斤亚麻):植物油8g,NaOH2g、洗涤剂9g,200g的水搅拌调制成乳化液,然后放入温度为60℃的仓中52h。利用带有针齿的开松机械对堆仓后的亚麻纤维进行初步开松后,再将其喂入梳棉机中进行进一步的开松、分劈,梳棉机给棉板抬高5.0cm,刺辊与给棉板隔距采用7.5mm。 Beat the flax into hemp and put it in the pickling pool, add 9 kg of water per kg of flax (bath ratio 1:9), add oxalic acid, the concentration of oxalic acid is 2.4g/L. Raise the temperature of the solution to 70°C, keep it warm for 70 minutes, take it out and wash the flax fiber with clean water, so that the pH value of the flax fiber reaches about 7; put the washed flax fiber into the oxidation solution, the bath ratio is 1:9, and oxidize The content of hydrogen peroxide (calculated as pure H 2 O 2 ) in the liquid is 10g/L, sodium silicate content 6g/L, sodium carbonate content 6g/L, urea content 7g/L, JFC content 3g/L. Raise the temperature of the oxidizing solution from room temperature to 95°C at a constant speed, and control the heating time at 45 minutes. After reaching the temperature, let the oxidizing solution keep warm for 3.5 hours; beat the oxidized flax fibers with a mallet for 5 times; The flax fiber is cleaned to wash away the medicines and impurities remaining on the surface of the fiber. Use a centrifugal dehydrator to dehydrate the flax fiber. After dehydration, in the emulsified oil soaked in the flax fiber, use 27g of white oil, 2g of NaOH, and 9.5g of detergent per kilogram of flax fiber, stir with 9kg of water to form an emulsion, and impregnate the flax fiber in it. Incubate at 70°C for 2 hours. The oiled fibers are dehydrated and dried by a dryer. The dried flax fiber is processed through a flax softening machine and sprayed with an emulsion. Its composition is (per kilogram of flax): 8g of vegetable oil, 2g of NaOH, 9g of detergent, and 200g of water are stirred to form an emulsion, and then put into a temperature of 52h in a warehouse at 60°C. Use the opening machine with pin teeth to initially open the flax fiber after stacking, and then feed it into the carding machine for further opening and splitting. The carding machine raises the cotton board by 5.0cm , The gap between the licker-in roller and the cotton feeding board is 7.5mm.
采用以上工艺制备的精细化亚麻纤维的主要性能指标如下: The main performance indicators of the refined flax fiber prepared by the above process are as follows:
表8、实施例8制备的亚麻纤维主要性能指标 Table 8, main performance index of flax fiber prepared by embodiment 8
实施例9: Embodiment 9:
将亚麻打成麻放入浸酸池中,每公斤亚麻用水11公斤(浴比1∶11),加入硫酸,硫酸浓度为3.0g/L。将溶液温度升至60℃,保温50min后取出用清水对亚麻纤维进行清洗,使亚麻纤维的pH值达到7左右;将清洗后的亚麻纤维放入氧化液中,浴比采用1∶11,氧化液中双氧水(按纯按纯H2O2算)含量为11g/L,硅酸钠含量7g/L,碳酸钾含量5g/L,尿素含量8g/L,JFC含量4g/L。将氧化液的温度由常温匀速升至97℃,升温时间控制在50min,温度到达后让氧化液保温3.8h;用木槌对氧化后的亚麻纤维进行敲打,打击5次;用清水对敲打后的亚麻纤维进行清洗,洗去残留在纤维表面的药品和杂质。利用离心脱水机将亚麻纤维脱水,脱水后将亚麻纤维浸泡的乳化油中,每公斤亚麻纤维用白油35g,NaOH7g、洗涤剂9.0g,与水11kg搅拌形成乳化液,将亚麻纤维浸渍其中,在90℃的环境下保温2.5h。将给油后的纤维脱水,经烘干机烘干。烘干后的亚麻纤维经过软麻机加工,并喷上乳化液,其成分为(每公斤亚麻):植物油30g,NaOH7g、洗涤剂11g,180g的水搅拌调制成乳化液,然后放入温度为55℃的仓中15h。利用带有针齿的开松机械对堆仓后的亚麻纤维进行初步开松后,再将其喂入梳棉机中进行进一步的开松、分劈,梳棉机给棉板抬高4.0cm,刺辊与给棉板隔距采用6.5mm。 Beat the flax into hemp and put it in the pickling pool, add 11 kg of water per kg of flax (bath ratio 1:11), add sulfuric acid, the concentration of sulfuric acid is 3.0g/L. Raise the temperature of the solution to 60°C, keep it warm for 50 minutes, take it out and wash the flax fiber with clean water, so that the pH value of the flax fiber reaches about 7; put the washed flax fiber into the oxidation solution, the bath ratio is 1:11, The content of hydrogen peroxide ( calculated as pure H2O2 ) in the solution is 11g/L, sodium silicate content is 7g/L, potassium carbonate content is 5g/L, urea content is 8g/L, and JFC content is 4g/L. Raise the temperature of the oxidizing solution from room temperature to 97°C at a constant speed, and control the heating time at 50 minutes. After the temperature reaches, let the oxidizing solution keep warm for 3.8 hours; beat the oxidized flax fibers with a wooden mallet for 5 times; The flax fiber is cleaned to wash away the medicines and impurities remaining on the surface of the fiber. Use a centrifugal dehydrator to dehydrate the flax fiber. After dehydration, in the emulsified oil soaked in the flax fiber, use 35g of white oil, 7g of NaOH, and 9.0g of detergent per kilogram of flax fiber, stir with 11kg of water to form an emulsion, and impregnate the flax fiber in it. Incubate at 90°C for 2.5 hours. The oiled fibers are dehydrated and dried by a dryer. The flax fibers after drying are processed by a softening machine and sprayed with an emulsion. The composition is (per kilogram of flax): 30g of vegetable oil, 7g of NaOH, 11g of detergent, and 180g of water are stirred to form an emulsion, and then put into the emulsion at a temperature of 15h in a warehouse at 55°C. Use the opening machine with pin teeth to initially open the flax fiber after stacking, and then feed it into the carding machine for further opening and splitting. The carding machine raises the cotton board by 4.0cm , The gap between the licker-in roller and the cotton feeding board is 6.5mm.
采用以上工艺制备的精细化亚麻纤维的主要性能指标如下: The main performance indicators of the refined flax fiber prepared by the above process are as follows:
表9、实施例9制备的亚麻纤维主要性能指标 Table 9, main performance index of flax fiber prepared by embodiment 9
实施例10: Embodiment 10:
将亚麻打成麻放入浸酸池中,每公斤亚麻用水12公斤(浴比1∶12),加入草酸,草酸浓度为2.8g/L。将溶液温度升至65℃,保温80min后取出用清水对亚麻纤维进行清洗,使亚麻纤维的pH值达到7左右;将清洗后的亚麻纤维放入氧化液中,浴比采用1∶12,氧化液中双氧水(按纯按纯H2O2算)含量为12g/L,硅酸钠含量8g/L,碳酸钾含量6g/L,尿素含量6.5g/L,JFC含量4g/L。将氧化液的温度由常温匀速升至100℃,升温时间控制在60min,温度到达后让氧化液保温4.0h;用木槌对氧化后的亚麻纤维进行敲打,打击5次;用清水对敲打后的亚麻纤维进行清洗,洗去残留在纤维表面的药品和杂质。利用离心脱水机将亚麻纤维脱水,脱水后将亚麻纤维浸泡的乳化油中,每公斤亚麻纤维用白油40g,NaOH8g、洗涤剂10.0g,与水12kg搅 拌形成乳化液,将亚麻纤维浸渍其中,在100℃的环境下保温0.5h。将给油后的纤维脱水,经烘干机烘干。烘干后的亚麻纤维经过软麻机加工,并喷上乳化液,其成分为(每公斤亚麻):植物油40g,NaOH10g、洗涤剂12g,60g的水搅拌调制成乳化液,然后放入温度为50℃的仓中20h。利用带有针齿的开松机械对堆仓后的亚麻纤维进行初步开松后,再将其喂入梳棉机中进行进一步的开松、分劈,梳棉机给棉板抬高4.5cm,刺辊与给棉板隔距采用0.1mm。 Beat the flax into hemp and put it in the pickling pool, add 12 kg of water per kg of flax (bath ratio 1:12), add oxalic acid, the concentration of oxalic acid is 2.8g/L. Raise the temperature of the solution to 65°C, take it out after 80 minutes of heat preservation, and wash the flax fiber with clean water, so that the pH value of the flax fiber reaches about 7; put the washed flax fiber into the oxidation solution, the bath ratio is 1:12, and oxidize The content of hydrogen peroxide (calculated as pure H 2 O 2 ) in the liquid is 12g/L, sodium silicate content 8g/L, potassium carbonate content 6g/L, urea content 6.5g/L, JFC content 4g/L. Raise the temperature of the oxidizing solution from room temperature to 100°C at a constant speed, and control the heating time at 60 minutes. After the temperature reaches, let the oxidizing solution keep warm for 4.0 hours; beat the oxidized flax fibers with a wooden mallet for 5 times; The flax fiber is cleaned to wash away the medicines and impurities remaining on the surface of the fiber. Use a centrifugal dehydrator to dehydrate the flax fiber. After dehydration, in the emulsified oil soaked in the flax fiber, use 40g of white oil, 8g of NaOH, and 10.0g of detergent per kilogram of flax fiber, stir with 12kg of water to form an emulsion, and soak the flax fiber in it. Incubate at 100°C for 0.5h. The oiled fibers are dehydrated and dried by a dryer. The flax fibers after drying are processed by a flax softening machine and sprayed with an emulsion. The ingredients are (per kilogram of flax): 40g of vegetable oil, 10g of NaOH, 12g of detergent, and 60g of water are stirred to form an emulsion, and then placed in a temperature of 20h in a warehouse at 50°C. Use the opening machine with pin teeth to initially open the flax fiber after stacking, and then feed it into the carding machine for further opening and splitting. The carding machine raises the cotton board by 4.5cm , The gap between the licker-in roller and the cotton feeding board is 0.1mm.
采用以上工艺制备的精细化亚麻纤维的主要性能指标如下: The main performance indicators of the refined flax fiber prepared by the above process are as follows:
表10、实施例10制备的亚麻纤维主要性能指标 Table 10, main performance index of flax fiber prepared by embodiment 10
将上述经过精细化处理的亚麻纤维进行纺纱加工。 Spinning the refined flax fiber. the
实施例11 Example 11
所制取的亚麻纤维通过如下纺纱流程纺制高支亚麻纤维纯纺和混纺纱: The prepared flax fiber is spun into high-count flax fiber pure spinning and blended yarn through the following spinning process:
纯纺:开清→梳棉→(预并→精梳)→并条→粗纱→细纱→后加工。 Pure spinning: cleaning→carding→(pre-combing→combing)→drawing→roving→spinning→post-processing. the
→并条2→粗纱→细纱→后加工。 →Drawing 2→Roving→Spinning→Post-processing. the
注:上述流程中,预并→精梳工序在纺高支纱(纯纺50公支以上,混纺60公支以上)时采用;纺60公支以下的麻/棉纱时,棉可以不精梳;化纤都不经过精梳。 Note: In the above process, the pre-merging → combing process is used when spinning high-count yarns (pure spinning above 50 public counts, blended spinning above 60 public counts); when spinning hemp/cotton yarns below 60 public counts, the cotton may not be combed; Chemical fibers are not combed. the
精细化亚麻纤维纯纺纱其主要质量指标如下: The main quality indicators of refined flax fiber pure spinning are as follows:
表11、实施例11制备的亚麻纯纺纱主要性能指标 Table 11, main performance index of flax pure spinning prepared by embodiment 11
精细化亚麻纤维混纺纱其主要质量指标如下: The main quality indicators of refined flax fiber blended yarn are as follows:
表12、实施例11制备的亚麻混纺纱主要性能指标 Table 12, the main performance indicators of the flax blended yarn prepared in Example 11
实施例12 Example 12
所制取的亚麻纤维通过苎麻纺纱工艺流程纺制亚麻/苎麻混纺纱: The prepared flax fiber is spun into flax/ramie blended yarn through the ramie spinning process:
表13、实施例12制备的36公支的亚麻50/苎麻50纯混纺纱主要性能指标 Table 13, the main performance indicators of the 36 public count flax 50/ramie 50 pure blended yarns prepared in Example 12
本发明还提供若干比较例,以说明本发明所述的制备方法具有优势: The present invention also provides some comparative examples, to illustrate that the preparation method of the present invention has advantages:
比较例1 Comparative example 1
表14、不同方法制备的亚麻纤维主要性能指标 Table 14. Main performance indicators of flax fibers prepared by different methods
其中1为按照专利申请88102614实施例1方法制备; Wherein 1 is prepared according to the method of Example 1 of patent application 88102614;
其中2为按照专利申请200610031004实施例1方法制备; Wherein 2 is prepared according to the method of Example 1 of patent application 200610031004;
其中3为按照专利申请200610031004实施例2方法制备; Wherein 3 is prepared according to the method of embodiment 2 of patent application 200610031004;
其中4为按照本发明实施例4方法制备。 Wherein 4 is prepared according to the method of Example 4 of the present invention. the
比较例2 Comparative example 2
本比较例说明采取不同氧化参数对产品质量的影响,本比较例是按照实施例1方法,并对具体参数进行调整。当考察一个参数时,其它参数固定不变。譬如当考察碳酸钠用量的影响时,其它参数如硅酸钠、尿素等均采用已经确定的本发明方案中的某个固定值。 This comparative example illustrates the influence of different oxidation parameters on product quality. This comparative example is according to the method of Example 1, and specific parameters are adjusted. When examining one parameter, the other parameters are held constant. For example, when investigating the influence of sodium carbonate consumption, other parameters such as sodium silicate, urea etc. all adopt a certain fixed value in the scheme of the present invention that has been determined. the
表15、不同氧化参数对亚麻纤维细度的影响(Nm) Table 15. Effect of different oxidation parameters on flax fiber fineness (Nm)
以上数据说明,当采用本发明制备方法,能够制备细度高的亚麻纤维,且优选方案得到的亚麻纤维具有更高的细度。 The above data shows that when the preparation method of the present invention is adopted, flax fibers with high fineness can be prepared, and the flax fibers obtained by the preferred scheme have higher fineness. the
表16、不同氧化参数对亚麻纤维断裂强度的影响(cN/tex) Table 16. Effect of different oxidation parameters on the breaking strength of flax fibers (cN/tex)
以上数据说明,当采用本发明制备方法,能够制备高强度的亚麻纤维,且优选方案得到的亚麻纤维具有更高的强度。 The above data shows that when the preparation method of the present invention is adopted, high-strength flax fibers can be prepared, and the flax fibers obtained by the preferred scheme have higher strength. the
此外,本发明所述技术方案的各项参数的范围都一一分别进行组合实验,无论参数如何组合进行,得到的纤维强度、细度均可符合上述的规律,即本发明技术方案所述的参数范围无论如何组合,得到的亚麻纤维性能均优于范围之外的参数,而优选的参数范围得到的亚麻纤维性能又可得以进一步提升。由于篇幅所限,本发明对于其他组合的实验数据不再一一列举。 In addition, the ranges of the various parameters of the technical solution of the present invention are combined and tested one by one. No matter how the parameters are combined, the obtained fiber strength and fineness can conform to the above-mentioned rules, that is, the technical solution of the present invention. No matter how the parameter ranges are combined, the properties of the obtained flax fibers are better than the parameters outside the range, and the properties of the flax fibers obtained in the preferred parameter ranges can be further improved. Due to limited space, the present invention will not list the experimental data of other combinations one by one. the
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CN102888659B (en) * | 2012-11-05 | 2015-01-07 | 东华大学 | Preparation method of polygonum multiflorum fiber used for spinning |
CN102925990A (en) * | 2012-11-13 | 2013-02-13 | 东华大学 | Method for pre-spinning chemical modification and degumming of linen fiber |
CN104630905A (en) * | 2015-01-28 | 2015-05-20 | 四川玉竹麻业有限公司 | Fibrilia oil supply emulsion and preparation method thereof |
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CN109402783A (en) * | 2018-11-07 | 2019-03-01 | 华祥(中国)高纤有限公司 | A kind of imitative flax fiber, preparation method and applications |
CN112267294A (en) * | 2020-11-09 | 2021-01-26 | 苏州纳昇源新材料科技有限公司 | Preparation method of multi-scale cellulose nano-fiber based on flax fiber |
CN115198523B (en) * | 2022-07-21 | 2023-08-22 | 东华大学 | Flax short fiber dry spinning oil-feeding humidifying health-preserving process |
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